In this paper a sequential experimental program used for model discrimination and parameter estimation of kinetic models for the high temperature-shift reaction over "B109" catalyst is presented.
本文介绍了应用序贯实验设计方法对“B109”型催化剂中温变换反应动力学竞争模型进行模型筛选及参数估计的过程。
Through model screening and parameter estimation, a kinetic model of cyclohexane steam reforming reaction is obtained.
通过模型筛选和参数估值，得到了环己烷水蒸汽转化反应动力学模型。
The reaction took place in the fixed bed reactor. By using steady state model, each step kinetic parameter in the reaction net was acquired.
反应是在固定床的条件下进行的，通过建立稳态反应模型，求出了异构化反应网络中的每一步动力学参数。
The reaction took place in the fixed bed reactor. By using steady state model, each step kinetic parameter in the reaction net was acquired.
反应是在固定床的条件下进行的，通过建立稳态反应模型，求出了异构化反应网络中的每一步动力学参数。
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